Method for sheathing a cable core with the core surrounded by impregnating fluid during sheathing

ABSTRACT

A process for sheathing a cable core with metal in which the core is immersed in oil in a container and is transferred from the container to the sheath extruder in a siphon tube in which oil flows in a direction opposite to the direction of movement of the core. From the extruder, the metal sheathed core is transferred to a drum and during such transfer the core is subjected to oil under pressure. Prior to inserting the core in the siphon tube, the latter is evacuated and filled with degassed oil. The apparatus comprises a stainless steel siphon tube with one end in the container and the other end connected to the extruder. The siphon tube has a higher intermediate portion to which a piezometric column and a pump are connected and has a coupling adjacent the extruder for supplying degassed oil to the siphon tube.

2 Unite States Patent [19] [111 3,918,281

Priaroggia Nov. 11, 1975 [5 METHOD FOR SHEATHING A CABLE 3,876,4644/1975 McNerney 156/48 ffigfggggg ggggggfi BY FOREIGN PATENTS ORAPPLICATIONS SHEATHING 1,217,738 12/1970 United Kingdom 156/48 71,234,396 6/1971 United Kingdom 156/48 lnventQ Paolo Gazzana PriaroggiaMilan 1,234,397 6/1971 United Kingdom 156/48 ltaly Primary ExamineF- C.W. Lanham [73] Assignee. Industrle Plrelli S.p.A., Milan, ItalyAssistant Examiner Ef M. Combs [22] Filed: Oct. 24, 1974 Attorney,Agent, or Firm-Brooks Haidt Haffner & 21 Appl. No.2 517,789 Delahumy 57AB TRACT [30] Foreign Application Priority Data 1 l S Nov 21 1973 {ml 31497 [73 A process for sheathing a cable core with metal In y which thecore is immersed in oil in a container and is [52] U S Cl 72/38, 29/20272/46 transferred from the container to the sheath extruder 72/25'8, 156/48 in a siphon tube in which oil flows in a direction oppo- [51] IntC12 Bzlc 23/30 HolB 13/24 site to the direction of movement of the core.From [58] Fie'ld 72/38 258 the extruder, the metal sheathed core istransferred to 29/202 5 156248 1 a drum and during such transfer thecore is subjected to oil under pressure. Prior to inserting the core inthe [56] References Cited siphon tube, the latter is evacuated andfilled with degassed oil. The apparatus comprises a stainless steelUNITED STATES PATENTS siphon tube with one end in the container and the2.115.574 /1 38 Gas other end connected to the extruder. The siphon tubegrlfiroggla el has a higher intermediate portion to which a piezometriccolumn and a pump are connected and has a 5:22:32: et coupling adjacentthe extruder for supplying degassed 3,444,016 5/1969 Baskwell 156/48 011to the slpho tube' 3,514,349 5/1970 Shiroya et a1. 156/48 3,854,44412/1974 Franke et a1 156/48 5 Clalms, Drawmg Figures METHOD FORSHEATHING A CABLE CORE WITH THE CORE SURROUNDED BY IMPREGNATING FLUIDDURING SHEA'THING The present invention relates to a process andapparatus for covering a core impregnated with fluid oil with a metalsheath which are particularly useful for manufacturing submarine cablesof long length and without joints. As used herein, the term core means aconductor, generally insulated with cellulose paper and preferably, butnot necessarily, wrapped with metallized cloth.

In the known processes for the formation of oil-filled cables having ametal sheath outer covering, the core is first collected in coils in apan in the shape of a toroidal container situated in a closed autoclaveand is dried under high vacuum and then impregnated. After impregnation,the core is immersed in the pan or tank in a degassed oil bath and undera head, namely, is submersed for about ten centimeters under the surfaceof the bath. At this time the autoclave is opened, the pan is removedand is transferred, together with the core contained therein, to aposition upstream of an extrusion press, i,e., apparatus able to extrudea metal sheath, for example, oflead or aluminum over the core.

From this point, the core to be sheathed passes to the extruder througha siphon tube connected at one end to the extruder by means of avacuum-tight connection tube which extends to the mandrel of theextruder. In said process, a piezometric column, where vacuum has beenpreviously created, is situated at the highest point of the siphonsystem, and in general, is connected to it by means of a check valve. Atthe top of the piezometric column the high vacuum is applied whichpermits the carrying out of that stage in the sheathing process which inthe present description is defined as first stage or treatment stage.Such stage comprises subjecting the system for transferring the corefrom the immersion bath to the sheath extrusion position to a highvacuum. The expression transferring system means herein at least thesiphon tube connected to the piezometric column, at least a portion ofthe extruder and the length of cable having an extruded sheath thereonand having a sealed end, which will be described hereinafter. The vacuumtreatment consists essentially of a series of operations intended toeliminate almost all traces of air or moisture from the transferringsystem.

In said known processes, when the extruder has been started and beginsto operate, a plug connected at one end to a drawing rope and connectedto the cable extremity at the other end is caused to pass into thesiphon tube a distance sufficient to reach the sheath to be extruded,with which it engages. At this time, the check valve connecting thepiezometric column to the siphon tube is opened and a turbulent mass ofoil and foam flows up the siphon tube to the piezometric column andprimes it, so that the oil coming from the immersion bath flows towardsthe vacuum-tight tube connected to the extruder and the tube of extrudedmetal until they are filled. After a few minutes the foam disappears,but unfortunately, this does not mean that all the air and moisturepreviously present in the transferring system are eliminated. On thecontrary, the risk of air and moisture absorption by the external paperswound around the core conductor remains a factor during the secondstage, or transferring stage, namely, from the time the core end isintroduced in the sheath,

and for the whole sheathing operation, until the sheathing of the coreis completed.

In some prior art embodiments, attempts have been made to minimize therisk of air and moisture absorption by the insulating paper of the coreby supplying degassed oil under pressure to the lower end of the corecoils, the expression lower meaning herein the core end opposite to thatsecured to the drawing rope. However, because of the permeability of thepaper, the oil passes through said paper, and after the passage thereofalong a core length of about 50 meters, the oil has already left the oilduct of the core and has passed into the tank containing the core coils.

The same unsatisfactory result is obtained with the weak stream ofdegassed oil coming from the feeding of oil to the drawing end of thecable which commences when the latter reaches the take-up bobbin orreel.

Moreover, in the system in use at present, the extruded sheath at theoutlet of the extruder and the stored cable downstream of the extruderalways is partially or totally situated at a level higher than the oilsurface level in the tank containing the core to be sheathed, andseriousdamage to the cable can result by undergoing a lowering ofpressure in the last stage of the sheathing process. The last stage isherein defined as a third stage, or completion stage, which is thatstage providing, in addition to the sheathing of the core, the storageof the finished cable.

The present invention has, as one object, the elimination of thedisadvantages described hereinbefore by providing a process, andapparatus for carrying out the process, by means of which it is possibleto produce sheathed cables devoid of any trace of gas even in longlengths.

More particularly, the principal object of the present invention is aprocess for the metal sheathing of an impregnated core, which comprisesa first stage in which the core transferring system which extends fromthe immersion bath to the sheath being extruded and provided with an endseal is subjected to a high vacuum, a second stage in which the core istransferred and a third stage in which the sheathed cable is completedand stored. The preferred embodiment of the invention comprises thefollowing steps:

1. in said first stage, a high vacuum is first produced in thetransferring system and subsequently, said system is supplied withdegassed fluid oil under pressure;

'2. in said second stage of transferring the core, after thetransferring system is filled with degassed fluid oil under pressure,said transferring system is connected under head with said immersionbath, the supply of degassed oil under pressure is continued until astrong, continuous stream directed from the transferring system to theimmersion bath is obtained, and then the core is pushed in thetransferring system in a sense opposite to the motion of said stream tofacilitate washing of the outer layers of the core insulation;

3. in said third or completion stage, the core is mechanically connectedto the metal sheath, and said core, as it is being covered with themetal sheath and stored on an appropriate means, is kept at a pressurehigher than the atmospheric pressure acting on the surface level of theoil bath.

A further object of the present invention is apparatus for carrying outthe process described hereinbefore, in which apparatus said transferringsystem is a siphon tube which is connected at its highest point to apiezometric tube which can be connected to a vacuum pump and whichsiphon tube is connected at one end with a vacuum-tight tube reachingthe mandrel of the extruder. Said siphon tube preferably is a tube ofstainless steel provided with a coupling for feeding thereto thedegassed oil under pressure, said tube having the opening at itsopposite, free end provided with a closing means which permits closingof such end in a vacuumtight manner before producing the high vacuumduring the first stage.

Other objects of the invention will be apparent from the followingdetailed description of a presently preferred embodiment of theinvention, which description should be considered in conjunction withthe accompanying drawings in which:

FIG. 1 is a diagrammatic, side elevation view of a plant formanufacturing a sheathed cable impregnated with fluid oil according tothe process of the invention;

FIG. 2 is a schematic diagram showing the circulation of the fluid oilin the plant before collecting the cable on a bobbin or reel; and

FIG. 3 is a schematic diagram showing the circulation of the fluid oilin the plant after collecting the already sheathed core on the bobbin.

A core 10, intended to form part of an electric cable impregnated withfluid oil, is at first collected in coils in a pan 11 which may, forexample, be a toroidal container of the type described in Italian Pat.No. 721,804

and the Patent of Addition No. 801,543. The core has previously beensituated in a closed autoclave (not shown) where it is dried under highvacuum and then impregnated with oil. After impregnation, the core 10 isimmersed in a bath of degassed fluid oil in the pan 11 and is placedunder the surface 120 of the oil 12 a distance of at least about 10centimeters, namely, with the highest point of the core 10 at at leastabout 10 centimeters below the surface 12a of the oil bath.

The pan 11, together with the core 10 arranged inside it, is thentransported by an appropriate means, for example, a crane (not shown) toa rotatable platform 13 situated upstream of the sheathing portion 14 ofthe plant.

The lower, or trailing, end of the core 10 is sealed in any suitablemanner and the other, or leading, end of the core 10 has an ogival shapein longitudinal crosssection so as to facilitate its passage into asiphon tube as described hereinafter.

The sheathing portion 14 of the plant comprises a siphon tube 15, avacuum-tight connection tube 16, a conventional extruder 17 forextruding a sheath of metal, e.g., lead or aluminum, over the core 10and at least a collecting bobbin or drum 18. The free end 19 of thesiphon tube 15 is in the oil 12 in the pan l1 and is provided with aclosing means 15b, for example, a plug which permits closing of its endin a vacuum-tight manner. The siphon tube 15 is preferably composed of atube of stainless steel having a specular inner surface, and the tube 16may be of the type shown and described in US. Pat. No. 2,981,409. Thecross-section of the siphon tube 15 has an inner diameter greater thanthe outer diameter of the core 10 and can have, for example, an innerdiameter which is double the outer diameter of the core 10.

The siphon tube 15 is provided with one or more elastic joints 20. In apreferred embodiment, the steel tube 15 is made from several tubularpieces joined together by flexible, corrugated tubular bodies (elasticjoints) which impart to the tube 15 a certain flexibility.

The siphon tube 15 is also supported, in one or more zones, byappropriate supports 15a, for example, of the trellis type, which permithorizontal and vertical dis placement of the tube 15. The other end 21of the siphon tube 15 is connected to the first free end of thevacuum-tight connecting tube 16, of a conventional type, provided at theextruder l7 and reaching the mandrel of the same.

It is to be noted that the output of the extruder 17 is at a heightabove the floor 30 which is less than the height of the surface 121: ofthe oil bath 12 so that it is below the upper level of the oil bath 12.The extruder 17 is suitable for extruding lead or aluminum, depending onwhether the cable is to be sheathed with one material or the other.

Downstream of the extruder 17, there is a suitable bobbin or drum 18 forcollecting or storing the cable 27 which comprises the core 10 coveredwith the metal sheath. The drum 18 has its highest point situated at alevel below the upper surface level 12a of the fluid oil 12 in the pan11.

Other apparatus, for example, a corrugator for the sheath, if this ismade of aluminum, a winding regulator, a cooling tank, etc., can beprovided, if necessary or desired, between the extruder l7 and the drum18.

A piezometric column 22 is connected to the siphon tube 15 at thehighest point of the siphon tube 15. Said column 22 is provided at itsupper end with a transparent sight tube 23 and a vacuum tank 24connected to a vacuum pump 25.

A coupling 26 is provided at one of the lowest points of the siphon tube15 upstream of the extruder 17 and in proximity to it. In particular,the coupling 26 is at a short distance from the free end of thevacuum-tight connection tube 16 of the extruder l7 and said coupling 26serves to connect the siphon tube 15 with a supply 31 of degassed oilcoming from a degasser 29 for the oil of the plant.

After having removed the pan 11 containing the core 10 from theautoclave where it has been dried and impregnated and placed the core onthe rotatable platform 13, the oil 12 covering the core 10 tends toabsorb air, but the core 10 is temporarily protected because it is underan oil head of preferably at least 10 centimeters.

At this point, the first stage of the process, that is, the stage oftreatment of the transferring system, is started. A short section 28 ofthe sheath is extruded and sealed at its outward end. The free end 19 ofthe siphon tube 15 is closed with the closing means 15b, e.g., a plug,and vacuum is created in the transferring system by means of the vacuumpump 25. The expression transferring system" means the portion 28 ofextruded sheath with its sealed end, the extruder 17, the vacuumtightconnecting tube 16, the siphon tube 15 and the piezometric column 22.

When the vacuum is appropriate, namely, is about 0.01 mm/Hg, degassedoil, coming from the supply 31 connected to the plant oil degasser 29,is sent to the siphon tube 15 through the coupling 26.

When the oil reaches a predetermined level in the piezometric tube 22and is visible through the transparent tube 23, while the supply ofdegassed oil through the coupling 26 is continued, the plug closing thefree end 19 of the siphon tube 15 is removed while said end 19 isimmersed under head in the oil 12 in the pan l1.

Degassed oil is therefore transferred to the pan 11 through the siphontube 15. The pan 11 is provided with one or more overflow outlets (notshown) situated in a position diametrically opposite to the free end 19.Such outlets send oil back to the degasser practically in the sameamount as is supplied to the transferring system.

In this way, a strong, continuous, closed-circuit circulation stream isproduced which, in about half-an-hour, is able to renew completely theoil 12 in the pan 11, thereby maintaining the oil degassing degree at anacceptable level. FIG. 2 illustrates diagrammatically the oil flow atthis time, and it will be noted that the oil circulates in a closedpath.

At this time it is possible to begin the step indicated in the presentdescription as the transferring stage, in which the operator takes theogival, leading end of the core and, while maintaining it under the oil12, pushes it into the siphon tube through the opening of the free end19,also under the oil 12. This preliminary operation of insertion of theend is facilitated by pushing it into the siphon tube 15 as the pan 11and the platform 13 are manually rotated. Then, the platform 13 isplaced into automatic, driven rotation, and the core 10, pushed by therotation of the pan 11 and aided by the ogival shape of its end, by thepresence of the extremely fluid oil in the siphon tube 15 and by thespecular inner surface of the latter, travels easily into the siphontube 15 until it reaches the vacuum-tight tube 16 and enters theextruder 17.

The continuous stream of the fluid oil provided as shown in the diagramof FIG. 2, meets the core 10 in a sense opposite to the motion of thelatter, namely, in counter-current thereto, and exerts a strong washingeffect on the outer layers of the insulation thereby removing the gastraces which may exist on the insulation. Such gas traces, in any case,would be very small because the core 10 does not come into contact withair and is protected by a layer of fluid oil 12 which is rapidly renewedby the oil flowing from the free end 19 of the siphon tube 15.

When the end of the core 10 reaches the extruder 17, the core 10 ispulled along in the extruder as it is covered with the metal sheath.

At this time, it is possible to begin the step defined in the presentdescription as third stage or completion stage. After having subjectedthe core 10 covered with the metal sheath to conventional processes asdesired, for example, after cooling and corrugation of the sheath, ifthis is made of aluminum, the metal sheath is mechanically connected tothe end of the core 10, namely, said sheath engages on the O-rings ofsaid end of the core 10 as described, for example, in US. Pat. No.3,342,162 and as indicated in US. Pat. No. 3,561,250. The excess portionof the sheath is then removed in order to open the cable oil duct whichis connected to the degasser 29, in a known manner, at the time at whichthe core 10 provided with the sheath, that is, the formed cable, beginsto be wound up on the drum 18. As illustrated in FIG. 3, such oil fromthe degasser 29, which has a head or pressure greater than that of theoil 12in the pan 11, passes through the central duct of the sheathedcable and then passes through the insulating papers into the tube 15,thereby increasing the counter-current of oil for washing the core 10 inthe siphon tube 15.

The plant of FIG. 1 illustrates the case in which the impregnation withfluid oil of the core 10, comprising at least a conductor and theinsulating papers, but preferably also provided with an outer winding ofmetallized cloth, has taken place in the toroidal container 11 immersedin a normal impregnation tank or autoclave and then, transported on therotatable platform 13 after impregnation. However, it is clear that thesame plant and the same process can be applied also when the treatmentof the core 10 and its subsequent impregnation take place on the samerotatable platform 13 supporting a toroidal container acting as animpregnation tank.

The pan type impregnating system is, however, the preferred one, sinceit affords the advantage of obtaining considerable savings with respectto the tank impregnation system. In fact, the former permits the pan 11to be left clean and can be immediately used for other impregnationcycles or for other impregnation systems, for example, with viscouscompounds rather than with fluid oil.

Although a preferred embodiment of the present invention has beendescribed and illustrated, it will be understood by those skilled in theart that various modifications may be made without departing from theprinciples of the invention.

What is claimed is:

l. A multi-stage process for sheathing an impregnated core having aconductor surroundedby insulation and at least one oil passageway insaid core, in which process the core is transferred from a container inwhich it is immersed in a degassed, water free liquid to an extruder atwhich the sheath is applied thereto as the sheathed core is then removedfrom the extruder, said core being surrounded intermediate saidcontainer and the point in said extruder at which the sheathed metal isapplied to the core by a housing which is fluidtight except at one ofits ends at said container and at its other end at said extruder, saidprocess comprising the following steps:

sealing said housing at its ends;

evacuating the gas from said housing;

filling said housing with a degassed oil under pressure;

opening said one end of said housing and placing it in said liquid insaid container to permit said oil to flow from said housing into saidcontainer,

at a point on said housing spaced from said container,

supplying said oil to said housing to cause it to flow from saidlast-mentioned point toward said container;

inserting one end of said core into said housing through said opening atsaid one end and moving said core along the inside of said housing tosaid other end of said housing; connecting said end of said core to asource of degassed oil under a pressure higher than the fluid pressureat said one end of said housing; and

while extruding metal of said sheath on said core,

moving said core through said housing in the direction away from saidcontainer and maintaining a supply of oil to said point on said housingand to said core to cause said oil to flow along said core duringmovement thereof and thereby remove gases which may be present in saidcore.

is supplied thereto through said housing, degassing the oil removed fromsaid container and supplying said last-mentioned oil to said point onsaid housing thereby to provide circulation of said oil in a closedcircuit.

5. A process as set forth in claim I, wherein said liquid is oil and isthe same as said degassed oil supplied to said point on said housing andsaid oil in said source connected to said end of said core.

1. A multi-stage process for sheathing an impregnated core having aconductor surrounded by insulation and at least one oil passageway insaid core, in which process the core is transferred from a container inwhich it is immersed in a degassed, water free liquid to an extruder atwhich the sheath is applied thereto as the sheathed core is then removedfrom the extruder, said core being surrounded intermediate saidcontainer and the point in said extruder at which the sheathed metal isapplied to the core by a housing which is fluid-tight except at one ofits ends at said container and at its other end at said extruder, saidprocess comprising the following steps: sealing said housing at itsends; evacuating the gas from said housing; filling said housing with adegassed oil under pressure; opening said one end of said housing andplacing it in said liquid in said container to permit said oil to flowfrom said housing into said container; at a point on said housing spacedfrom said container, supplying said oil to said housing to cause it toflow from said lastmentioned point toward said container; inserting oneend of said core into said housing through said opening at said one endand moving said core along the inside of said housing to said other endof said housing; connecting said end of said core to a source ofdegassed oil under a pressure higher than the fluid pressure at said oneend of said housing; and while extruding metal of said sheath on saidcore, moving said core through said housing in the direction away fromsaid container and maintaining a supply of oil to said point on saidhousing and to said core to cause said oil to flow along said coreduring movement thereof and thereby remove gases which may be present insaid core.
 2. A process as set forth in claim 1, wherein the gas isevacuated from said housing until the vacuum therein is at least about0.0l mm/Hg.
 3. A process as set forth in claim 1, wherein said point onsaid housing is intermediate said container and said extruder andadjacent to the latter.
 4. A process as set forth in claim 1, whereinsaid liquid is said oil and further comprising removing said oil fromsaid container at substantially the same rate as it is supplied theretothrough said housing, degassing the oil removed from said container andsupplying said last-mentioned oil to said point on said housing therebyto provide circulation of said oil in a closed circuit.
 5. A process asset forth in claim 1, wherein said liquid is oil and is the same as saiddegassed oil supplied to said point on said housing and said oil in saidsource connected to said end of said core.